report on batteries 04072014

8/18/2019 Report on Batteries 04072014

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Batteries and Supercapacitors for

Energy Storage and Delivery Needs of India

A report submitted to

Office of the Principal Scientific Advisor to the Government of India

New Delhi

2014


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CONTENTS

Page

Executive Summary 2

Preface 4

Abbreviations used in the text 5Contributors 6

1. Introduction 7

2. The Indian scene 9

2.1. The battery market 9

2.2. Manufacturing base 10

3. Electrochemical energy storage systems 11

4. Battery systems 11

4.1. Lead-acid batteries 11

4.2. Alkaline batteries 154.2.1. Nickel–iron battery 15

4.2.2. Iron–air battery 18

4.2.3. Nickel–metal hydride battery 20

4.3. Lithium-ion batteries 22

4.4. Redox flow batteries 24

4.4.1. The vanadium–vanadium redox flow battery 24

4.4.2. The soluble lead redox flow battery 25

4.5. Sodium–sulfur and zebra batteries 26

5. Electrochemical capacitors 27

5.1. Electrical double layer and pseudo-capacitors 27

5.2. The lead–carbon battery-supercapacitor hybrid 28

6. Indian strength in battery R&D 29

7. Multi-functionality in energy storage landscape 30

8. New materials, new tools 30

8.1. Nano-architectures, an answer? 31

8.2. Theory and modelling 32

9. Technology readiness level 33

10. Recommendations 34

11. Looking ahead 36

Bibliography 37


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Executive Summary

Batteries are important drivers of modern civilization, powering applications from mobile

phones to aircraft and strategic systems. The use of batteries is expected to further grow with the

emergence of electric mobility and increased use of hand-held electronic devices. Further, with

emphasis on renewable energy, which is intermittent, the demand for batteries from this segment

is likely to grow manifold to store and distribute energy and for integrating with existing systems.

Thus, batteries (chemical energy storage) and electrochemical capacitors (electrical energy

storage) are considered critical in meeting this requirement, as they are ideally suited to store

energy and release it on demand. Their reliability, safety, modularity and affordability makethem ideal for applications in sectors such as consumer electronics, telecommunication, medical

instrumentation, electric mobility, uninterrupted power supply, electric traction, grid power,

defence and space.

It is clear that the sustainability of a society depends on prudent generation and management

of electrical energy. With this in mind, the Office of the Principal Scientific Advisor to the

Government of India constituted a working group to draw a status report and a roadmap on

energy storage technologies for India. This report presents the status of the science and

technology of electrochemical energy storage systems as well as Indian expertise, manufacture

and market potential, and new directions that need to be pursued for a sustainable energy

management. There is a great deal of novel science and research coming from academic and

research centers, including on materials and system integration research. However, there is also a

growing technology/knowledge gap between the basic science and the battery manufacturing

environment that needs to be bridged. To this end, it is mandatory to bring researchers and other

experts from academia, government organizations, start-ups and battery manufacturing

companies to share knowledge and debate issues and find solutions to technical problems. A mix

of academia and industry will open opportunities to move concepts from laboratory to

commercialization. The present effort is to bridge the gap between research and production to

realize the next big leap in battery power.

This report focuses on both mature and emerging electrochemical energy storage technologies.

Technologies under discussion are lead-acid batteries, alkaline batteries (nickel–iron; iron–air;

nickel–metal hydride), lithium-based batteries (lithium-ion; lithium–air; lithium–sulfur), redox


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flow batteries (vanadium–vanadium; soluble-lead), high-temperature sodium batteries (sodium–

sulfur; zebra), and electrochemical capacitors (electrical double layer and pseudo-capacitors; lead–

carbon battery-supercapacitor hybrid).

The need for intensive investigations is emphasized by highlighting the fact that currenttechnologies fall short of the performance requirements expected for several existing as well as

emerging applications. Given the paucity of our understanding of molecular-level and interfacial

processes that are fundamental to the working and failure of these systems, it is necessary that the

systems be revisited with the aid of new analytical and characterization tools. Similarly, critical

technology gaps must be addressed through new synthetic and processing strategies, engineering

design and system modeling, and by pushing materials to their stability limits and tapping into

new knowledge on nano- and multi-functional materials. The Indian battery scene and

technology readiness levels of battery systems are also briefly discussed. The report culminates by

emphasizing the need for establishment of Centers of Excellence in electrochemical energy

technology and for putting in place a policy on sustainable energy with stakeholders drawn from

the academia, industry and government.


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Preface

Increasing reliance on renewable energy sources, and technological advances in areas such as

electric traction, smart grids and portable electronic gadgets have catalyzed renewed interest in

energy storage options. The electrochemical mode of energy storage offers flexibility and

scalability as well as candidate systems with a range of energy/power densities. With their low

costs and low rates of self-discharge, they are particularly suitable for stationary applications as in

power grids that are connected to intermittent renewable energy sources such as wind and solar.

Batteries are classified by chemistry, and the most common ones are lead-, nickel- and lithium-

based systems, which command 48, 10 and 37%, respectively, of the worldwide secondary battery

market share. The shares of all the other systems add up to just 5%. Batteries are a fast growing

market bolstered by the electronics manufacturing segment as well as by expanding production

and use of motor vehicles. The global demand for batteries is forecast to rise by 8.5% per year to

$144 billion in 2016.

Batteries are energy devices. Because energy and power play against each other, increasing

one will lead to a loss in the other. This means that if we require high power from a battery, we

will extract less total energy than when we require low power. Capacitors, being power devices,

complement battery power by allowing very rapid charge and discharge. Accordingly, capacitors

will gel well with batteries into the emerging energy-storage landscape. Since the capacitance

mode allows storage of electricity directly as electrical charges, electrical-double-layer capacitors

can have efficiencies close to 100%. Supercapacitors are a relatively newer technology with a

projected global market of $40 billion by 2020.

In a timely initiative, the Office of the Principal Scientific Advisor to the Government of India

constituted a committee of experts in electrochemical energy storage to draw a status report on

both mature and emerging electrochemical storage technologies and their suitability in meeting

the energy requirements of India in conjunction with energy efficiency, electricity delivery and

energy reliability to clearly define future requirements for energy storage from the perspective of

applications relevant to transportation as well as electricity distribution and identify critical

technology gaps. This report presents the status of the science and technology of electrochemical

energy storage systems as well as Indian expertise, manufacture and market potential, and new

directions that need to be pursued for a sustainable energy management.


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Abbreviations used in the text

3D three-dimensional

AC alternating current

AGM absorbent glass mat

ARCI International Advanced Research Centre for Powder Metallurgy and New

Materials

CECRI Central Electrochemical Research Institute

CNT carbon nanotube

CoE Center of Excellence

DC direct current

EDLC electrical double layer capacitor

EV electric vehicle

HER hydrogen evolution reaction

HEV hybrid electric vehicleICEV internal combustion engine vehicle

IISc Indian Institute of Science

MH metal hydride

NMEM National Electric Mobility Mission

OER oxygen evolution reaction

ORR oxygen reduction reaction

PANI polyaniline

SLI starting–lighting–ignition

Super NiCad Super nickel–cadmium battery

TRL technology readiness levelUPS uninterrupted power supply

VRLAB valve-regulated lead-acid (VRLA) batteries

ZEBRA Zeolite Battery Research Africa


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ontributors

A.K. Shukla, Indian Institute of Science, Bangalore.

T. Prem Kumar, Central Electrochemical Research Institute, Karaikudi.

N. Munichandraiah, Indian Institute of Science, Bangalore.

B.C. Chakraborty, Naval Materials Research Laboratory, Ambernath.

S. Venugopalan, People’s Education Society of Technology, Bangalore.

K.S.N. Murthy, Amara Raja Batteries Limited, Tirupati.

A.S. Nagaraj, NED Energy Limited, Hyderabad.

D. Yogeswara Rao, Office of the Principal Scientific Advisor to the Government of India,

New Delhi


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1. Introduction

Batteries are important drivers of modern civilization, powering application from mobile

phones to aircraft to strategic systems. Batteries enable us to start our cars, communicate

with smart-phones and tablets and power our pacemakers. Batteries are also a key

technology for electric-mobility and the new energy economy, suggesting that these chemical

energy stores are soon going to be game changers.

With the world electricity consumption expected to grow at 3.6% annually, increasing

emphasis is being placed on more efficient technologies with low or zero-carbon footprints

for both generation and use of energy. India is embarking on ambitious solar and wind

energy projects. The energy from both these sources is, however, intermittent. It is, therefore,

necessary to store the energy generated from these sources for continuous supply. Thus,

electrical storage technologies are called upon for both storing excess power and for meeting

peak-power demands. Indeed, experts consider storage batteries seminal to the success of

renewable energy programs.

Uninterrupted power supply (UPS) is another area that begs attention. Power shortage

and associated problems such as low frequency, tripping of generators and load shedding are a

bane of state electricity boards. Low-cost imports from China and Taiwan as well as high

domestic cost of raw materials are major challenges for the manufacturers. The proliferating

digital world is a major consumer of UPS batteries.

Electric traction is another area that promises a humongous growth market for batteries.

India is also a growing market in this sector. However, battery cost is a hurdle to widespread

penetration of electric vehicles. Thus, in order to encourage proliferation of electric vehicles,

the Ministry of New and Renewable Energy provides financial incentives: Rs 4,000 for low-

speed electric two-wheelers, Rs 5,000 for high-speed electric two-wheelers, Rs 60,000 for

seven-seater three-wheelers, and Rs 100,000 for electric cars manufactured in India. Not

surprisingly, therefore, several players have entered the fray, some prominent ones being

Ampere Vehicles, Hero Ultra, Yo Bikes, ACE Motors, Eko Vehicles, Go Green, Reva, Hero

Electric, Mahindra & Mahindra, Mitsubishi, and Tata. Under the National Electric Mobility

Mission Plan 2020 (NMEM 2020), 6–7 million electric vehicles are expected to be on the

road.


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Storage and release of electrical energy is unarguably critical for uninterrupted and non-

fluctuating supply with increasing penetration of intermittent renewable power sources.

However, only a handful of back-up storage technologies are efficient and at the same time

economical. If additional requirements such as sustainability and low-carbon emissions are to

be factored in, the choices narrow down to such technologies as pumped-storage

hydroelectricity, which, however, comes with the burden of location, environmental

conservation and social problems. Other leading energy storage technologies include

flywheels, superconducting magnetic energy storage, compressed air energy storage, water

electrolysis and methanation, and electrochemical energy storage devices such as batteries

and electrochemical capacitors.

Several of these technologies have a fast response time, which is essential if power

blackout during peak demand is to be avoided. However, high installation costs and poor

efficiency as with water electrolysis and methanation can hamper their widespread use. They

must also have low rates of self-discharge. Flywheel and superconducting magnetic energy

storage technologies suffer from self-discharge rates of 3–20% per hour and about 12% per

day, respectively. By contrast, the self-discharge loss in lead-acid batteries, for example, is

only about 5% per month. Batteries and electrochemical capacitors can be cost-effective and

allow for flexibility in deployment, which can in turn facilitate widespread use and

networking of intermittent renewable energy technologies. Electrochemical storage

technologies are also ideal for transportation where instant power should be available for the

vehicle for reasonable lengths of time. They are also mature, inexpensive and ensure high

levels of safety, reliability and durability. They are ubiquitous, coming in various sizes and

capacities, suitable for stationary and portable applications in a broad spectrum of human

activity.

It is noteworthy that the dramatic explosion of the portable electronics market owes much

to the ubiquitous batteries that power them. However, the days of the conventional battery

systems seem numbered. The performance levels of conventional batteries are often found

wanting for projected applications, be it in the burgeoning electronics industry or in the

transportation sector, where a shift in gears from the internal combustion engine vehicles

(ICEVs) to electrically operated vehicles is on the cards. A common sight on the roads at theturn of the century, battery operated cars, which were pushed out of the race by superior


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ICEVs, made a transient resurgence in the 1970s as a result of the first oil-shock. However,

today, a rebirth of the electric vehicle is both necessary and imminent. Today, we are

addicted to oil and seem settled in the cozy comfort of the gas-guzzling ICEVs albeit being

confronted by a number of issues such as geo-politics and the consequent oil price wars and

disruptions in the supply of petroleum products, the longevity of petroleum resources, and

stricter policies on climate change and vehicular emissions. In the battle for alternative fuels

for a decarbonized transportation sector, electricity has a definite edge. There is, however, a

lingering fear that battery technology has not lived up to the demands of the electric vehicle.

Although an immediate choice is the plug-in hybrid electric vehicle, the ultimate goal is an

all-electric vehicle. This goal is a major driver in the search for electrochemical storage

technologies that are not only radically different from existing ones but also outperform

them, for the stakes are too many.

Ranked the tenth largest economy today, India is expected to break into the third position

after the US and China. However, its per capita income is not anywhere near those of

developed countries. The situation, therefore, demands that high-quality products are made

available at low prices. For example, the Government of India’s intervention to transform the

automotive paradigm from the one based on fossil fuels to electric traction (NMEM 2020) is

estimated to cost it Rs 13,000–14,000 crore in the next 5–6 years. While the mission aims to

reduce carbon dioxide emissions by 1.3–1.5%, what is overlooked is the fact that bulk of the

money that the common man spends on his new electric vehicle will be on the battery pack!

There is thus an urgent need to strengthen our base on the expertise and manufacturability of

affordable power systems.

This report seeks to discuss all of these issues relating to battery technologies and provides

a road map for India.

2. Indian scene

2.1. The battery market

The world demand for primary and secondary batteries is expected to rise by 8.5% per year,

accounting for a $144 billion market in 2016. China will remain the largest and fastest

growing market, while the growth of battery market in India will be relatively slower. Thegrowth curve has new contributors other than the portable electronics sector, which includes


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grid storage systems based on renewables, electric vehicles, and high-drain electronic gadgets.

In the coming years, advanced lead-acid, nickel–metal hydride and lithium-ion batteries are

expected to make further forays into specialized applications. Developing nations such as

India will register greater market impact due to increasing demands and industrialization.

The lead-acid battery market in India is dominated by Exide and Amararaja, which command

as much as 70% of the $4 billion Indian market.

2.2. Manufacturing base

India has a world-class manufacturing base for lead-acid batteries. The lead-acid battery

market is well established in India. Major players in the organized sector include Amararaja

Batteries, Exide Industries, Hyderabad Batteries, NED Energy and Tata Green with the lion ’s

share coming from the first two. There is also a mushrooming unorganized lead-acid battery

sector, thriving on borrowed art, catering to a wide section of customers. CECRI has

established a national battery testing center, which today caters only to the lead-acid battery

industry. The infrastructure, resources, expertise and support base from allied industries can

come in handy for launching new related systems such as the lead-carbon hybrid battery and

the soluble lead redox flow battery. The many now-defunct nickel–cadmium battery units

can easily be transformed into manufacturing units for the nickel–iron, iron–air and nickel–

metal hydride batteries. This sharply contrasts with the nearly non-existent infrastructure

available for lithium-ion battery manufacture.

In January 2013, India had 862.62 million mobile phone subscribers, which is just one

application area for lithium-ion batteries. Surprisingly, for a country that boasts of 862.6

million mobile subscribers, India does not have even a single manufacturing base for lithium-

ion batteries. It must be noted in passing that Future Hitech Batteries Limited, which is a rebirth

of the Twenty First Century Battery Limited, has inherited an obsolete technology from

Bellcore. Indocel Technologies is one company that imports cells from their principals,

assembles batteries of required specifications complete with battery management systems,

and supplies to targeted customers. Apart from the high initial investments, especially in

specialized facilities such as dry rooms, the challenges in adopting new methodologies

relating to rapidly-emerging battery chemistries also pose a problem to potential investors.Bereft of a conducive manufacturing platform, India is ill-prepared to push forward with


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establishment of this battery technology. It is time policy makers identified core

challenges related to lithium battery manufacturing.

3. Electrochemical energy storage systems

There are two types of electrochemical energy storage systems: (i) batteries that store energy

as chemical energy in their active materials (chemical storage), and (ii) electrochemical

capacitors that store energy as charge (capacitive storage). Currently available

electrochemical storage technologies fall short of projected day-to-day requirements, as for

example for electric vehicles, in terms of their energy and power densities, and even in terms

of the time they take to get recharged. Our understanding of the fundamental and inter-

related processes that govern their operation, performance, safety limits and failure remains

alarmingly poor even after two hundred years of the demonstration of the first galvanic cell

by Alessandro Volta. Much needs to be researched before we can translate our understanding

of the fundamental molecular processes into practical devices.

In this report, we review the current status of electrochemical energy storage technologies

and their limitations, and address key directions and new materials that can lead to high-

performance energy storage devices. The individual systems chosen for discussion areconsidered mature and emerging, suitable for a sustainable future, and adequate enough to

meet the needs of the Indian populace.

4. Battery systems

4.1. Lead-acid batteries

A mature technology, the lead-acid battery is backed by 150 years of development. With less

than $150/kWh, lead-acid batteries are unrivalled in terms of cost-effectiveness. Today, lead-

acid batteries command more than half of a whopping $60 billion world battery market, with

India’s share of the market being about $4 billion, out of which the share for automotive

batteries is Rs 10,000 crore while that for industrial batteries is Rs 10,000 crore. The lead-acid

market is projected to grow by 5–20% in various application sectors in the coming years.

Lead-acid batteries are commonly used for starting-lighting-ignition (SLI), deep cycling and

stand-by applications.


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The battery operates on the double-sulfate reaction in which both the active materials,

spongy lead in the negative plate and lead oxide in the positive plate, are reversibly converted

into lead sulfate. During discharge, lead dioxide and lead react with sulfuric acid to form a

non-conducting solid product of lead sulfate. Both the discharge reactions are accompanied

by an increase in the volume of the solid phases: the volume increase for the transformation

of PbO2 to PbSO4 is 92%, while that for Pb to PbSO4 is 164%.

There are three types of lead-acid batteries in common use: (a) batteries with flooded

electrolyte, (b) flooded-electrolyte low-maintenance lead-acid batteries with a large excess of

electrolyte, and (c) batteries with immobilized electrolyte and a pressure-sensitive (safety)

valve, usually referred to as valve-regulated lead-acid (VRLA) batteries. Normal flooded-

electrolyte batteries use lead-antimony alloy positive grids. Their water consumption, which

is low in the initial stages, increases as much as five times toward the end of their lives. The

low-maintenance-type flooded-electrolyte batteries use low antimony alloy positive grids.

Such batteries with calcium alloy grids consume only about one-tenth the water needed by

equivalent sized antimony cells. In these batteries, the water requirement is low and

constant throughout their lives. VRLA batteries, based on the oxygen recombination cycle,

do not vent gases and do not require periodic topping. Moreover, these batteries offer

freedom of battery placement, increased safety, and superior performance. Their cycle life

and deep discharge capability depend on the type of construction. In flooded-electrolyte

lead-acid batteries, the electrolyte is filled to a level above the top of the plates and bus bars.

This has the disadvantage that the cells have to be vented to release the gases liberated during

charging, namely, oxygen at the positive plate and hydrogen at the negative. The

consequence of this venting is that the batteries have to be used only in the upright position;

otherwise leakage of electrolyte takes place. Also, the released gases carry a very fine mist of

acid, which is highly corrosive. The seepage of acid on the top cover of the battery leads to a

leakage current, resulting in increased self-discharge and ground-shunting. The latter is a

process by which the battery drains itself by grounding or by discharging through a grounded

body, as for example of an electric car. The flooded-electrolyte lead-acid battery requires

checking of specific gravity of the electrolyte, periodic addition of water to maintain

electrolyte level above the top of the plates, and recharge soon after the battery discharge tomitigate hard sulfation that causes loss in battery capacity. On the other hand, VRLA


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batteries, based on the oxygen recombination cycle, do not vent gases and do not require

periodic topping. Moreover, these batteries offer freedom of battery placement, increased

safety, and superior performance. Valve-regulated versions of the lead-acid battery are

sensitive to temperature and cyclic applications.

Commercially available lead-acid batteries have specific energies of 25–40 Wh/kg (60–75

Wh/l). Their discharge-charge watt-hour efficiencies lie between 80 and 85%. Despite the

fact that their current energy densities are rather low and their cyclability only of the order

of a few hundreds of cycles, they remain the preferred workhorse for a variety of applications

where weight and volume are secondary. The flooded-electrolyte lead-acid batteries are the

traditional types used in stationary applications although the VRLABs are now increasingly

being used. The latter use an absorbent glass mat (AGM) or a gelled mass as the electrolyte

and have a compacted stack construction. Continual improvements in design and use of

alloying additives have resulted in VRLABs with a higher shelf-life and cycle-life.

Contrary to popular belief, scientists have come to recognize that there is more to be

expected from lead-acid batteries. In fact, until not long ago, they were stereotyped with the

common SLI batteries, whose performance expectations are limited. The entry of high-

energy batteries such as nickel–metal hydride and lithium-ion batteries triggered research on

tapping deeper into the performance capabilities of lead-acid batteries. Electrode reactions in

lead-acid batteries give rise to several products with differing morphologies. Deep-

discharges, as expected in applications such as electric vehicles, would mean maximizing

volume and morphological changes in the active materials, a consequence of which is

shedding of the active mass. Deep-discharge and failure to routinely return to full state-of-

charge lead to sulfation of the negative plate. Abusive overcharge also leads to corrosion of

the positive plate. In stationary applications such as power grids and roof-top photovoltaic

installations, erratic regimes may be expected.

In recent years, the science and technology of lead-acid batteries has seen a paradigm

change, opening up possibilities in higher-energy-density applications. For example, both

mechanical properties and corrosion resistance of lead grids have been improved by the use of

alloying additives. A debilitating phenomenon in lead-acid batteries is sulfation, which is

now sought to be mitigated by use of a thin layer of carbon in the negative plate. In fact, theresults have been so dramatic that Honda replaced the nickel–metal hydride batteries in its


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Insight HEVs with these batteries. Other recent developments include 3D polysiloxane-

based gel electrolytes as well as separators and light-weight-current collectors. To retain the

market position, to withstand the persistent tough competition from other technologies,

several innovations have been made in the technology of lead-acid batteries that include (a)

lead-carbon ultrabatteries, (b) bipolar lead-acid batteries, (c) soluble-lead redox flow

batteries, (d) substrate-integrated lead-carbon supercapacitors, (e) thin-plate pure-lead lead-

acid batteries, (f) tri-polar lead-acid batteries, (g) strap-grid tubular positive lead-acid

batteries, (h) carbon composite foam current collector lead-acid batteries, (i) reticulated

vitreous carbon current collector lead-acid batteries, (j) lead-infiltrated ceramic bipolar-plate

lead-acid batteries, and (k) synthetic-fiber-reinforced AGM lead-acid batteries.

An Indian lead-acid battery industry has acquired know-how on carbon composite foam

current collector lead-acid batteries from Firefly Energy in the US. Atraverda is developing

Table 1. Performance benefits against improvements in lead-acid battery technology.

Technology Performance benefits

BipolarDramatic reduction in the number of battery components; low volume and weight;

higher energy and power densities; low mass of lead per kWh.

Tripolar Good high temperature performance; good rate capability.

Substrate-integrated

lead-carbonHigh power density; supports partial SOC operation; good high rate charge.

Strapgrid tubularImproved power output; good charge acceptance; best suited for VRLA with AGM

separator.

Carbon foam current

collector

High energy and power densities; good cycle life; composite plate material is lighter,

longer-lasting, with high active material utilization; foam negative plates give

performance comparable to Ni-MH, but at lower manufacturing costs.

RVC current

collectorHigh energy and power densities; good cycle life and high-rate performance.

Lead-infiltrated

ceramic bipolar plateHigh energy and power densities; good cycle life and high-rate performance.

Thin plate pure lead Good rate capability.

Synthetic fiber

reinforced AGM

Good tensile strength and puncture-resistance; minimal short circuit during assembly;

good resistance to oxidation especially at elevated temperatures; improved battery

life.

Enhanced flooded

lead acid batteryGood deep discharge cycle

Lead-carbon

ultrabattery

High power density; long cycle life; supports partial SOC operation; good high rate

charge acceptance; good low temperature cranking.

Soluble redox flow

battery

Employs a single electrolyte; operates without separator.


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new bipolar lead-acid batteries for the Indian market that will be smaller, lighter and more

environmentally-friendly. Raman FibreScience in Mysore has initiated manufacturing of

synthetic fiber-reinforced separators for lead-acid batteries. In brief, the Indian lead-acid

battery is trying to adopt the state-of-the-art technology.

Lead-acid batteries operate over a wide temperature range, between –20oC to +50oC. Lead

is toxic, but lead-acid batteries can be recycled with 99% recovery of lead. Two key issues

that have restricted wider commercial adaptability of lead-acid batteries are their low cycle-

life and limited specific energy. Performance benefits accrued by adoption of improvements

in the lead-acid battery technology are presented in Table 1.

4.2. Alkaline batteries

Alkaline batteries based invariably on the nickel oxyhydroxide cathode are superior to the

lead-acid battery in terms of energy turnover, ability to deliver continuous power, fast

recharge capability and long service-life. The nickel–iron battery was extensively deployed

in the railway carriages of the erstwhile Soviet Union. The instability of the iron electrode in

alkaline medium put the lid on the nickel–iron battery technology. The most popular among

alkaline batteries is the nickel–cadmium system, which dominated the market for several

decades. SAFT Batteries have commissioned the world’s biggest nickel–cadmium battery

bank (40 MW; 13,760 cells) for stationary applications in Alaska. An undesirable

characteristic of nickel–cadmium batteries, especially those with sintered-type cadmium

electrodes, is memory effect. Furthermore, their ability to recharge is limited by their

substantial negative temperature-coefficient. Their self-discharge rates are also high. These,

together with the toxicity of cadmium, have led to a waning in the production of nickel–

cadmium batteries worldwide. By contrast, nickel–metal hydride batteries have shown

promise in hybrid electric vehicles albeit being expensive and prone to heavy self-discharge.

At present, the Indian market share for nickel-based batteries stands at about US $ 30 million.

4.2.1. Nickel –iron battery

In hibernation for decades, the nickel–iron system has begun to catch the attention of policy

makers. The resurrection of the system rests heavily on its techno-economic feasibility for anumber of applications arising out of recent technological developments. Two problem areas


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that are being addressed are: (i) catalytic recombination of hydrogen and oxygen gases that

are evolved in the battery, with possibilities of a sealed battery, and (ii) electrolyte/electrode

additives that can shift the overvoltage for the hydrogen evolution reaction (HER). Latching

on to the new developments should propel nickel–iron battery for applications wherefrom

lead-acid and nickel–cadmium batteries have been withdrawn. Its cost competitiveness is

obvious considering its longevity, typically 3,000 cycles, corresponding to a calendar life of

about 20 years. Particular areas of application should include stationary ones as in

photovoltaic installations, where its mechanical robustness and long life even under adverse

operational conditions such as over-charge, over-discharge, charge-stand, discharge-stand

and inadequate maintenance would be very attractive.

The discharge reactions of the iron electrode proceed in two steps, yielding Fe(OH) 2 in the

first discharge step and FeOOH in the second. The open-circuit potential of the charged

alkaline iron electrode is always cathodic to the potential for HER in the same solution,

which renders the metal thermodynamically unstable. But the extraordinary robustness and

service life are appealing for civilian applications. The nickel cathode is a well-established

system. Under shallow discharge regimes, the nickel electrode is known to sustain more than

20,000 cycles as in Super NiCad batteries for space applications. The degree of utilization of

the nickel electrode varies from about 60% for pocket plate or pressed plate electrodes to

more than 90% for sintered plate electrodes. Freshly charged nickel electrodes lose 0.1–0.2%

capacity a day by self-discharge at 25C, which may be reduced with additives such as CdO.

Cycling the iron electrode is fraught with problems of poor charging efficiency (50–70%) and

low electrode utilization. Therefore, to offset the loss and to achieve satisfactory

performance, iron electrodes are typically overcharged by 60–100%.

Under the tropical conditions prevailing in India, where ambient temperatures can cross

even over 45C, it is preferable to use an electrolyte composition of 18% NaOH and 0.8–1.0%

LiOH (instead of the commonly employed 25% KOH + 1.0–1.2% LiOH). The less expensive

NaOH-based electrolyte sustains a larger number of cycles under high ambient temperatures

prevailing in India although that advantage comes with a small penalty in terms of a slightly

reduced nominal capacity. NaOH has a lower molecular weight than KOH and is also used at

a lower concentration, which give an additional advantage of a lowered battery-weight.


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Recently, the beneficial effect of sulfide additives on the cyclability of the iron electrodes

has been demonstrated, with a utilization efficiency of 68% of the rated capacity at 1C rate.

However, full exploitation of the system rests on control of the wasteful evolution of

hydrogen during charging. It was also shown that in situ electro-deposited bismuth led to

substantial inhibition of the kinetics of HER. The hydrogen evolution that occurs during

charging lowers the round-trip energy efficiency and necessitates constant maintenance to

replenish lost water. The gas evolution would mean that the battery cannot be sealed.

Carbonation of the electrolyte is thus a serious concern. It is clear, therefore, that

suppression of the evolution of hydrogen and sealability of the nickel–iron system have far-

reaching ramifications not only in raising the overall energy efficiency and lowering the cost,

but also in facilitating its penetration in various spheres of application. Recently, a nickel–

iron cell with a recombination catalyst was reported that paves the way for the development

of a sealed version of the battery.

Another concern with these batteries is their poor high-rate discharge performance.

Several applications such as electric vehicles and grid-scale energy storage demand battery

discharge at C or C/2 rates. It is found that a combination of high-purity α -iron incorporated

with bismuth by electro-reduction of bismuth sulphide exhibits a ten-fold decrease in

hydrogen evolution rate without interfering with the kinetics of the iron electrode reactions.

It is reported that an unprecedented 96% charging efficiency at a specific capacity of 400

mAh/g for the iron electrode and a twenty-fold increase in capacity at C/2 rate is now

achievable. These breakthroughs in the technology of the alkaline iron electrode should

augur well for large-scale exploitation.

Scientists at Stanford University constructed a nickel–iron battery with iron oxide grown

on graphene as the anode and nickel hydroxide deposited on multi-walled carbon nanotubes

as the cathode. The nano-configuration displayed a dramatic improvement in performance: it

could be fully charged in about two minutes and discharged in less than 30 seconds. This is a

jump of more than 1,000 times over the conventional rates of charging and discharging. The

new nanomaterial-based technology opens up opportunities especially in electric traction.

Because the battery allows fast charging and discharging, one would be tempted to put it to

more frequent use, like a supercapacitor.


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In recent years, interest in nickel–iron batteries is being revived since these batteries are

reliable and inexpensive, can be subjected to high discharge rates, exhibit good low- and

high-temperature behavior with long cycle life, can undergo two-step charge-discharge, can

provide reserve charge during the second step of discharge, are electrically and mechanically

rugged, and, above all, are environment-friendly. Today, it looks even feasible to assemble

nickel–iron batteries in sealed form by incorporating a gas-recombination catalyst. Its

suitability for India is also emphasized by the better performance of the system with

inexpensive NaOH-based electrolytes under high ambient temperatures. In fact, the

economics, eco-friendliness, longevity and performance of these systems are too favourable to

be dismissed under the euphoria of new inventions. It is high time that the Government of

India encouraged developmental efforts in these systems for public good.

4.2.2. Iron –air battery

Arguably, no battery can surpass the iron–air battery in terms of cost-competitiveness. The

battery has an additional advantage, characteristic of metal–air batteries, which is that the

cathode-active material (oxygen) need not be contained in the battery. Like the nickel–iron

battery, the iron–air battery also gives a two-plateau discharge curve. Although the open-

circuit voltage of the iron–air cell is 1.28 V, its working voltage is only 0.7–0.8 V.

The iron–air battery, first explored as a concept 40 years ago, is being revamped as an

inexpensive, rechargeable, high energy density power source. Once a prime candidate for

traction and military applications, they are now projected for large-scale energy storage and

as a candidate system that can accelerate the adoption of renewable energy sources. The

theoretical specific energy density of the iron–air battery is 955 Wh/kg, which is about three

times that of the nickel–iron battery and four times that of the lead-acid battery. The iron–air

system comes in two versions: electrically rechargeable and mechanically rechargeable. The

former has a lower specific energy than the latter, but the lower specific energy is somewhat

offset by the advantage of a lower life-cycle cost. The electrically rechargeable version may

have a bi-functional cathode or an auxiliary (third) electrode, which is used only for

recharging the battery. The alkaline iron anode does not suffer non-uniform and dendritic

metal deposition and shape change upon recharge.


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A notable disadvantage of metal–air batteries, however, is their poor energy efficiency

(around 50%). The realization of such batteries rests heavily on the development of a bi-

functional oxygen electrode and oxygen-selective membranes for mitigating carbonation of

the electrolyte. Besides their low cost, their environment-friendliness is a rallying point for

developmental activities in metal–air systems. It is now firmly believed that the future is in

the air.

The low solubility of oxygen in the electrolyte and the need to electrocatalyze the

reduction of oxygen at the three-phase zone (liquid–gas–solid interface) of the cathode

present unique problems especially on oxygen transport properties in the electrolyte. Thus,

the success of the electrically rechargeable iron–air battery rests solely on the perfection of

the air-breathing cathode. This means that electrochemical problems of intrinsically slow

reactions, high overpotentials and the poor reversibility of oxygen electrochemistry must also

be overcome. This requires the catalytic bi-functional air electrode to support both ORR

(oxygen reduction reaction) and OER (oxygen evolution reaction). Alkaline electrolytes

have a disadvantage that they absorb carbon dioxide in the air to form carbonates. The low

solubility of carbonates in alkaline media results in clogging of the pores of the air-breathing

cathode. It is thus necessary to feed purified air or use a membrane that is selectively

permeable to oxygen. A circulating electrolyte design may also be employed as saturation by

carbonate is attained much more slowly than with an immobilized electrolyte design.

ORR in alkaline solutions is favoured by fast kinetics and low overpotentials. On metal

surfaces, it can proceed via a four-electron or a two-electron pathway. While the four-

electron pathway generates OH– ions, the two-electron pathway leads to the formation of

peroxide ions. Direct transformation of oxygen to OH– ions by the four-electron pathway is

desirable due to its high energy efficiency. The peroxide species produced by the two-

electron pathway is corrosive and can lead to premature degradation of the cell.

Satisfactory rechargeability of the iron–air battery depends not only on the electrocatalysis

of the normally slow ORR during battery discharge, but also on accelerating the OER during

battery charging. It must be noted that for an efficient bi-functional air electrode, the

overpotentials for both ORR and OER should be minimal in order to maximize power output

and round-trip efficiency. Noble metals can electrocatalyze both ORR and OER, althoughtheir ability to sustain extended cycling is yet to be established. It is noteworthy that for


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widespread use of iron–air batteries, the technology should be based on cheap non-noble

metal catalysts only. Carbonaceous materials are among such inexpensive alternatives.

Vertically aligned nitrogen-doped carbon nanotubes have been shown not only to catalyze

the four-electron ORR, but also outperform Pt/C catalysts for ORR activity and durability.

Another class of non-noble ORR catalysts can be found in oxides, chalcogenides, nitrides and

carbides of transition metals. Manganese-based spinels and perovskites, in particular, exhibit

high activity and durability in alkaline electrolytes, and are among prime candidates as

catalysts for both ORR and OER. Other promising oxides include nanocrystalline Cox Mn3–

x O4 spinels, Co3O4 and Co3O4–N-doped reduced graphene oxide. Fundamental aspects of

electrocatalysis must be also revisited especially in the light of advancements in materials

electrochemistry. Modeling and computational quantum chemistry may lend a helping hand

in the design of such materials.

New avenues for exploitation lie in designing high-surface area nanostructured catalytic

surfaces and mimicking oxygen chemistries in Nature. Inspired by a cubane-like CaMn4Ox

active site, the biological catalyst found in the oxygen-evolving center in photosystem II, a

nanostructured Mn3O4 catalyst has been designed that exhibits ORR and OER properties

comparable to those of precious metal catalysts. Enzymes with redox-active sites capable of

supporting both ORR and OER could also be a biological answer to the bi-functional

electrode. In contrast to the rigid surfaces provided by inorganic solid catalysts, enzymes

present flexibility in redox sites and geometry. Nature can also be relied upon for designing

the air-breathing electrode. For example, respiratory organs such as human lungs and fish’s

gills allow efficient intake of oxygen at interfaces involving the solid, liquid and gas phases.

4.2.3. Nickel –metal hydride battery

Cadmium being toxic, alternatives to the nickel–cadmium system began to be explored,

which resulted in the nickel–metal hydride system. The nickel–metal hydride battery uses

alloys of AB2 (A: drawn from Ti, V, Zr, etc.; B: Ni, Co, Cr, Mn, Al, Sn, etc.) and AB5 (A: La,

Ce, Pr, Nd, or misch metal; B: Ni, Co, Mn, Al, etc.) compositions as the anode. Improvements

in the technology include use of a new A 2B7 composition and PEO-KOH gelled electrolyte

that ensure 80% coulombic efficiency. The cell reactions involve a cyclic transfer of protonsbetween the metal hydride (MH) anode and the NiOOH cathode.


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Although nickel–metal hydride batteries have been popular power sources for consumer

electronics and electric traction, it is only recently that they began to be considered for UPS

and telecommunication. A major disadvantage of nickel–metal hydride batteries is their high

rates of self-discharge (typically 30% per month). Moreover, its discharge-charge watt-hour

efficiency is only about 80%. Both nickel–metal hydride and nickel–cadmium systems have

similar cell voltages, but the former is free from memory effect. They have moderately high

specific energies and tolerate temperatures up to 70oC, a trait that not many other systems can

boast of. Despite its superior performance characteristics over the nickel–cadmium system,

nickel–metal hydride batteries are up against lithium-ion batteries in competing for a share of

the market.

Vehicular traction is one single application area where alkaline batteries hold promise due

to high power capability and long endurance both in terms of cyclability and service life. For

example, these batteries have been demonstrated to endure 10 years service in automobiles

and more than 200,000 running km. Developments in this direction include replacement of

the sintered nickel electrode with a foam electrode, bringing about 50% improvement in

volumetric capacity. Recent resort to highly porous foam electrodes and new varieties of

high-density nickel hydroxides has helped raise the volumetric charge density from 450 Ah/l

for the sintered electrode to 700 Ah/l for the foam electrode. Similarly, a 30% increase in

volumetric charge density has been achieved by simple replacement of the sintered cadmium

electrode with a cadmium slurry electrode. Other developments include use of thin

separators, new electrode designs and electrolyte compositions, all of which have brought

about substantial improvements in the performance of the battery.

Today, the use of nickel–cadmium batteries is limited to special applications where nickel–

metal hydride batteries would be found unsuitable. India is blessed with huge deposits of rare

earth elements all along its southern coastal belt. Therefore, cost considerations that have put

a brake on its widespread use elsewhere may not be much of a constraint for India. This

sharply contrasts with the scenario for lithium-ion technologies that depend entirely on

imports for lithium metal and lithium chemicals. The metal components must be recycled for

sustaining this metal-rich technology as recovery procedures for nickel from spent batteries

are already established, although rarely practised. Lead times for manufacture can beshortened by re-activating defunct nickel–cadmium plants.


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4.3. Lithium-based batteries

Lithium-ion batteries in commerce contain a variety of cathode materials such as layered

lithiated transition metal oxides, lithium-manganese spinel oxide and lithium iron phosphate,

although the anode-active material is usually graphite. These batteries represent the cutting

edge of electrochemical science and technology today. Bestowed with energy densities of

150–200 Wh/kg, low self-discharge rates and nearly 100% discharge-charge efficiency, they

have already captured a sizeable and niche market in portable gadgets. Although considered

very expensive for applications such as transportation and grid storage, they are expected to

vie for these markets once their costs are brought down by mass production. A major portion

of the cost arises from specialized processing and assembly lines as well as from the adoption

of safety measures. As for environmental impact, technologies are available for recovering

transition metals such as cobalt from spent batteries. Lithium oxides and lithium salts can

also be recycled although their content in lithium-ion batteries is below 1% by weight.

Nevertheless, given that India is not blessed with major reserves of lithium, recycling the

metal from spent batteries should be a priority in the long run.

Current technologies aim at replacing the toxic and expensive cobalt in the electrodes with

low-cost and eco-friendly metals such as iron, manganese, titanium, etc. Low-cobalt

alternatives include LiNi0.8Co0.15Al0.05O2 and LiNi1/3Mn1/3Co1/3O2, spinel electrode materials

such as the high-voltage LiNi0.5Mn1.5O4, and olivines such as LiFePO4 and LiFe0.8Mn0.2PO4. A

major breakthrough was made by the introduction of LiFePO4 as a cathode and Li4Ti5O12 as

an anode. Systems based on the above two materials have lower voltages, which render them

safer. On the anode side, much headway has been made in realizing practical specific

capacities much above that of the conventional graphite. The new anode-active materials

include alloy anodes, conversion electrodes and silicon. Replacement of the carbon anode

with high-capacity silicon, especially in nanowire form, is attracting much attention. More

stable and non-flammable electrolytes, including ionic liquid-based ones, are being

investigated upon. Lithium-ion batteries have now become commonplace and are the choice

systems for grid storage, electric vehicles, telecommunication and photovoltaic applications.

The basic reactions in lithium-ion batteries may be explained taking the carbon-lithium

cobalt oxide couple as an example. Cells are assembled in the discharged state, which meansthat they must be charged before use. New chemistries based on lithium are emerging, which


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include the lithium–sulfur and lithium–air systems. A practical energy density of 350 Wh/kg

has already been demonstrated for the lithium–sulfur system. The lithium–sulfur system

could potentially double the specific energy of lithium-ion batteries and offer competitive

cost. Much ground needs to be covered before problems associated with cyclability of the

positive and negative electrodes are solved. Safer and long-lasting solid electrolytes are also

being investigated. If integrated in a lithium–air battery, they should give a practical energy

density of 1,700 Wh/kg. The importance of this system should be viewed from its theoretical

energy density of 13,516 Wh/kg, which surpasses the theoretical value of 13,343 Wh/kg for

gasoline. The realization of a practical lithium–air battery is even more formidable. There

are a multitude of technical challenges to its realization including cyclability of the lithium

anode, bi-functional electrodes for the rechargeable cathode, charge-discharge rate capability

of the cathode, identifying electrolyte compositions, and designing membranes permeable to

the electrolyte but impermeable to water and carbon dioxide.

Safety has been a recurring theme in lithium-ion batteries. The several recalls of products,

especially by manufacturers of laptops and automobiles, and more recently, the grounding of

Boeing’s Dreamliner fleet, have not helped penetration of this technology into large-scale

applications. While lithium-ion batteries come with built-in safety methodologies based on

shutdown separators and electrical/pressure interrupts (limited to 18650 cells), manufacturers

fall back mainly on the expensive and more reliable safety circuitry for ensuring safety of the

batteries. A complicating factor is the absence of uniform, standardized regulations for large

batteries. This arises from the very nature of lithium-ion battery technologies that rely on a

variety of active materials for their electrodes and even on a variety of electrolyte

formulations.

Safety concerns arise not only from the fact that lithium-ion batteries have highly

oxidizing and reducing materials but also because their designs have an inherent drawback of

poor heat dissipation. Furthermore, the potential ranges experienced in these cells are

beyond the thermodynamic stability windows of the electrolytes. The temperature of a cell is

determined by the heat balance between the amount of heat generated and that dissipated by

the cell. Above a certain temperature (130–150◦C), exothermic chemical reactions between

the electrodes and electrolyte begin, raising the internal temperature of the cell. If the heat isnot dissipated, the cell temperature will rise abnormally, accelerating the chemical reactions,


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and eventually leading to thermal runaway. Possible exothermic reactions that trigger

thermal runaway are: (i) thermal decomposition of the electrolyte; (ii) reduction of the

electrolyte by the anode; (iii) oxidation of the electrolyte by the cathode; (iv) thermal

decomposition of the anode and cathode; and (v) melting of the separator and the consequent

internal short. Lithium-ion batteries are designed for applications where size and weight are

a premium and, therefore, a lower thermal capacity is an unavoidable penalty. Thus, heat

dissipation in lithium-ion batteries turns out to be a major engineering challenge, especially

for those designed for high power applications.

4.4. Redox flow batteries

Redox flow batteries consist of two electrolytes each with a redox couple. The solutions,

stored in separate tanks, are pumped through a cell in which chemical energy associated with

the redox couples is converted to electrical energy. The most common of these redox couples

are based on vanadium–vanadium, vanadium–bromine, sulphur –bromine, zinc–bromine,

cerium–zinc, iron–chromium, and lead–lead. They have energy densities of about 35–50

Wh/kg only. However, they have a long operational life of about 40 years or tens of

thousands of discharge cycles. Their energy and power can be increased independently of

each other: energy by increasing the size of the electrolyte tank and power by increasing the

size of the cell. Several commercial plants are in operation for grid storage. Because flow

cells operate for decades on end and generate hardly any waste product, their environmental

impact is zero except probably during installation and dismantling. The vanadium–vanadium

redox flow battery (with V5+ /V4+ and V3+ /V2+ redox couples), the iron–chromium flow battery

(with Cr 3+ /Cr 2+ and Fe3+ /Fe2+ redox couples) and the soluble lead redox flow battery are among

candidate systems that must be pursued.

4.4.1. The vanadium –vanadium redox flow battery

One of the most popular redox flow batteries is the vanadium redox flow battery, which

exploits the ability of vanadium to exist in four oxidation states in solution. An added

advantage of this property is that there is only one active element in both anolyte and

catholyte, which greatly reduces chances of cross-contamination of the anolyte and catholyte.The vanadium-vanadium redox flow battery is an excellent candidate for large-scale


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stationary storage. It consists of an assembly of power cells that contain an active electrolyte

of vanadium in dilute sulphuric acid. An ion–permeable membrane separates the two half-

cells. Electrochemical reactions take place on inert carbon felt electrodes from which the

current is collected. The rest of the battery assembly consists of mechanical components such

as pipes, pumps and flow tanks. The electrolyte has an indefinite life and is reusable.

4.4.2. Soluble –lead redox flow battery

One of the offshoots of the science and technology of lead-acid batteries is the soluble lead

redox flow battery, a system that offers potential cost and lifetime advantages. In this system,

the active lead is present as a single electrolyte, which eliminates the need for separator or

membrane, simplifying the cell design and reducing cost. A further reduction in cost and

battery weight is achieved by use of carbon-based electrodes instead of lead-based ones. In

addition, the improved resistance to sulfation and corrosion of carbon-based electrodes can

lead to extended cycle life.

The battery is based on the electrode reactions of lead(II) in methanesulfonic acid. During

cell charging, the soluble lead species are converted into a solid phase, with the reverse

reactions occurring during discharge. The lead redox flow battery differs from the lead-acid

battery both in concept and potential market. It is easy to see that the former represents a

quantum jump from the small box-type lead-acid batteries, catering particularly to large-scale

storage applications. At the laboratory scale, the lead redox flow battery exhibits a coulombic

efficiency of >85% and an energy efficiency of ~65%.

A critical issue in the long-term operation of this system is the chemical balance, which

must be restored on completion of a full charge/discharge cycle. However, restoration of the

electrodes and the electrolyte in their original states after repeated cycling can happen only if

the current efficiencies for the deposition/dissolution of lead and lead dioxide are the same.

This means that there should be little gas evolution and current efficiencies at the two

electrodes should be close to 100%. A few other challenges also remain to be tackled before

this system can be made practical. One of them is the crystalline form in which lead dioxide

is deposited upon recharge. Lead dioxide is known to occur in two polymorphs: α -PbO2

(orthorhombic) and β-PbO2 (tetragonal). Because the two phases have different physicalproperties, control of the structure of the deposited PbO2 is crucial to the performance and


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lifetime of the flow cell. Furthermore, the reversibility of the deposited PbO2 material is a

major performance-limiting factor. With increased cycle number, the amount of PbO2 that

remains on the cathode also increases, depleting the electrolyte of Pb2+ ions available for

subsequent charging of the cell. Over time, the energy storage capacity of the cell gets

diminished. On the anode side, lead can deposit as dendrites capable of shorting a cell in

bipolar stack architecture.

The formation of dendritic lead, PbO2 creep and PbO2 sledging have been identified as

possible failure modes, all resulting in electrical shorting between the positive and negative

electrodes. Growth of dendritic lead is observed under high current charging and discharging.

PbO2 creep can eventually bridge inter-electrode gaps. PbO2 sludges can build up in areas of

low electrolyte flow and through sedimentation onto horizontal cell components such as

electrode spacers and inlet manifolds.

4.5. Sodium–sulfur and zebra batteries

The key to success of the molten sodium-based batteries is a solid membrane of β-Al2O3 (often

doped with Li+ or Mg2+) with excellent sodium ion conductivity at elevated temperatures.

Operating at 300–350◦

C, the sodium–sulfur battery gives an energy density of 140–170 Wh/kg

at an average voltage of 1.78–2.08 V. The battery was originally developed for electric

vehicle applications, but fell behind in the mid-1990s with the emergence of competing

technologies such as the nickel–metal hydride. However, mega-watt installations still

operate for power grid applications, the largest being a 34-MW/238-MWh (7 h) unit for the

Rokkasho wind farm in Japan.

Replacement of the sulfur electrode in sodium–sulfur batteries with a cathode made of

porous metal/metal halide impregnated with molten NaAlCl4 results in ZEBRA (Zeolite

Battery Research Africa) batteries. The replacement renders it safer than the sodium–sulfur

battery. The usual metal halides are NiCl2 and FeCl2, yielding voltages of 2.58 and 2.35 V,

respectively. The higher voltages translate to higher energy densities than that for the

sodium-sulfur system. They also tolerate overcharge and over-discharge. ZEBRA batteries

have been demonstrated for transportation and stationary applications. The present cost of

these batteries is around $500-600/kWh.


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5. Electrochemical capacitors

5.1. Electrical double layer and pseudo-capacitors

The electrical double-layer at the electrode/electrolyte interface stores electrostatic energy

like a capacitor. The energy stored per unit area in the interface became technologically

attractive with the introduction of materials with high active-surface-areas, such as activated

carbons. The two parallel regions of charge in the interface are in molecular dimensions of

less than 10–9 m. With carbons of surface areas of about 1,000 m2 /g, this creates a capacitor

with specific capacitance of about 105 F/kg and possibly leading to devices rated at thousands

of farads. Owing to their appreciably high capacitance, these capacitors are also referred to as

supercapacitors or ultracapacitors. It is noteworthy that although supercapacitors are at least

10-fold lower in mass and volume, they have much slower response times, typically 0.3–3 s.

This precludes their use in alternating current filtering applications, making them, unlike

conventional capacitors, effectively direct current devices. Whilst the operation of EDLCs is

based on non-faradaic accumulation of electrostatic charge at the electrolyte/carbon surface,

fast faradaic charge-transfer brought about by the charging of the electrical double-layer at

the electrode/electrolyte interface determines the working of pseudocapacitors. A

combination of faradaic and non-faradaic components would generate electrochemical

capacitors that exhibit high capacitance for pulse power as well as sustained energy; these

electrochemical capacitors are referred to as hybrid supercapacitors.

Although power density values for a supercapacitor happen to be much higher than those

for batteries, the latter have energy densities much higher than the electrochemical

capacitors. Accordingly, electrochemical capacitors are categorized as power devices whilst

batteries are energy devices. Typically, energy density values for an electrochemical

capacitor are


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batteries have been used in electric vehicles, where the former provides peak power for

acceleration during hill climbing while the latter operates in a continuous low power-regime.

The combined action improves reliability, longevity and performance of the power system.

Carbon-based electrochemical double layer capacitors exhibit high power densities (100–

2,000 W/kg) but low energy densities (1–5 Wh/kg). Their typical discharge periods are

between 1 s to 1 min. Since the charge and discharge processes are purely physical

phenomena and involve no chemical changes, wear is low; they sustain hundreds of

thousands of cycles and last for more than 15 years. They are especially suitable for

instantaneous voltage compensation. Thus, batteries and electrochemical capacitors are

complementary power sources. For example, in electric vehicle batteries can provide power

for continuous drive while electrochemical capacitors can provide sudden bursts of power for

acceleration and hill-climbing. The latter are also amenable to energy storage by regenerative

braking.

Noble-metal oxides exhibit capacitances of about 700 F/g, but they are prohibitively costly

and are sought to be replaced with transition metal oxides and non-oxides such as Ni(OH) 2,

MnO2 and PbO2. Targeted research goals include increased lifetime, higher rated voltage,

wider range of operating temperatures, higher combined power/energy density, and

capacitance of the order of 1,000 F/g. Polymer-based supercapacitors, such as those based on

bithiophene–triarylamine, are attractive as they give a peak specific capacitance of more than

990 F/g, but problems of swelling and contraction, leading to mechanical degradation and

failure, as well as chemical degradation over repeated cycling must be addressed.

Incorporation of CNTs in these electrodes can mitigate degradation caused by volume

changes by reducing diffusion lengths. For example, a PANI/CNT composite electrode with a

hierarchical porous nanostructure gave a specific capacitance of 1,030 F/g.

5.2. The lead–carbon battery-supercapacitor hybrid

The recognition that carbon added in small amounts (0.15–0.25 wt.%) into the negative paste

of lead-acid batteries has been known to resist accumulation of lead sulfate led to a new class

of energy storage devices: the lead–carbon asymmetric supercapacitors. The new

configuration not only ensures higher cycle life, but also reduced sulfation of the positiveelectrode because of diminished swings in acid concentration during charging and


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discharging. This system is also sealable like a VRLAB. Moreover, it can be operated over a

wider depth-of-discharge window than conventional lead-acid batteries and can be charged

and discharged at higher rates. The new technology can replace the conventional lead-acid

system in applications such as in power grids. Its penetration is expected to be facilitated by

the fact that essentially the same manufacturing infrastructure required for lead-acid batteries

could be used for the new hybrid system.

6. Indian strength in battery R D

Given the versatility and varied chemistries that form the basis of practical battery systems,

the available expertise can shape up into ideal technology platforms for forays into specific

applications. India has a rich blend of expertise in the science and technology of

electrochemical storage systems. The contributions from the Indian Institute of Science need

special mention for realization of space-quality nickel–cadmium batteries at the Indian Space

Research Organization and, in recent years, for up-gradation of lead-acid battery technology

at NED Energy.

India boasts of world-class expertise in materials science and electrochemistry, vital for

battery technology. However, efforts and funding for battery research have largely been

piecemeal, which explains why no tangible products result from such programs. Today, a

bulk of battery researchers has joined the bandwagon of lithium-ion batteries. Pockets

specializing in lithium-ion batteries are the Central Electrochemical Research Institute,

Karaikudi, Indian Institute of Science, Bangalore, Indian Institutes of Technology in Mumbai,

Hyderabad and Kharagpur, Central Glass and Ceramics Research Institute, Kolkata,

Pondicherry University, Puducherry, PSG College of Technology, Coimbatore and the Indian

Institute of Science Education and Research, Thiruvananthapuram. Under the National Solar

Mission project, CECRI is poised for a leap in its infrastructure for battery assembly and

testing. The Indian Institute of Science is actively engaged in building a technology platform

for storage batteries with its Energy Storage Systems Initiative. The International Advanced

Research Centre for Powder Metallurgy and New Materials, Hyderabad and Naval Science &

Technological Laboratory, Vishakahpatnam have also invested huge sums for lithium-ion

battery research and development. Bharat Electronics Limited, Pune has also initiated somework in this area and Vikram Sarabhai Space Centre, Thiruvananthapuram is gathering


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expertise to assemble space-grade lithium-ion cells up to 100 Ah. For research in lead-acid

and nickel–iron batteries, only IISc can be counted upon. IISc has also successfully developed

and demonstrated the first substrate-integrated lead-carbon hybrid ultracapacitor that has

shown potential for commercialization. CECRI has acquired workable knowledge on nickel–

metal hydride batteries. It should, however, be borne in mind that nickel–metal hydride

batteries will become cost competitive to lithium-ion batteries only if India exploits its rich

resources of rare-earth metals.

7. Multi-functionality in energy storage landscape

Technological advances in areas as disparate as portable electronic gadgetry, electric vehicles

and the electrical grid are often hamstrung by limitations of the power pack. Moreover,

modern devices come with increasing multi-functionality. For example, today’s mobile

phones are transceivers of textual, voice and visual content with added capabilities for voice

recording, photography, data storage and transmission, and multi-media entertainment. So

much so, the power-on-demand profiles of applications become unpredictable, stretching

over a large time scale as well as a large swathe of the energy/power spectrum. This requires

power packs to be algorithm-controlled, multi-capable units with a balanced mix of batteries

and electrochemical capacitors. Such battery-electrochemical capacitor combinations should

effectively wrap up the entire energy-power-time range, helping to blur the restrictions

imposed by Ragone plots. Such a judicious technology mix will also guarantee supply

security and cost efficiency for a range of applications. Naturally, an area of research that is

gaining momentum is asymmetric supercapacitor configurations that address the energy-

power gulf between batteries and conventional capacitors. Specifically, these devices are

based on large-area transition metal oxide electrodes that support rapid and reversible

faradaic reactions in non-aqueous media that can operate at voltages much above 1.2 V.

8. New materials, new tools

Approaches to battery systems with higher performance should focus on: (i) new materials

and new chemistries, and (ii) improving the performance of existing systems. It is

noteworthy that the push for batteries with higher energy and power densities would meanpushing the active materials and electrolytes to their stability limits. This also would mean a


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penalty in terms of safety, reliability and charge-discharge cyclability, three crucial factors

that determine the acceptability of the device. While higher energy densities would require

any new battery-active material to possess higher specific capacities and/or to form galvanic

couples with higher cell voltages, cell safety and durability would require more stable

electrode-electrolyte interphases. Batteries exhibit high energy densities, but their power

densities are low. By contrast, electrochemical capacitors have low energy densities, but high

power densities. Thus, batteries and electrochemical capacitors complement each other in

the energy-power equation. In addition, the latter deliver high pulse currents and sustain

extended cycling. One way to enhance the energy densities of electrochemical capacitors is

to resort to new materials with enhanced capacitive properties. However, a key priority in

both the cases is the identification of highly conducting electrolyte solutions with wide

electrochemical stability windows and capable of forming stable interphases with the active

materials.

8.1. Nano-architectures, an answer?

There is increasing evidence that electrochemical energy storage devices stand to gain from

the rapidly strengthening nexus between electrochemistry and nanoscale science. A notable

feature of this nexus is that a number of materials that have hitherto been dismissed as

electrochemically inactive are now emerging as hot favourites to replace existing active

materials in batteries. Particular mention must be made of the demonstration of nano-SiO2

and nano-SiC as potential low-cost and high-capacity anode materials in lithium-ion

batteries. Conversion electrodes are another class of such materials that hold promise as

anodes that can deliver multiple electrons per molecular unit of the active material. Such

discoveries have opened the floodgates for systems that are projected as ‘beyond lithium’ and

‘beyond intercalation chemistry.’ The combination of electrochemistry and nanoscale

materials chemistry has also triggered research into pseudo-capacitance charge storage

materials. In fact, studies with nanostructured materials have led to the possibility of moving

towards the upper right quadrant of the Ragone plot, which erases the demarcation of

‘batteries for energy’ and ‘capacitors for power ’ model.

Tailored, multi-functional nano-architectures can enhance performance by way ofimproved electronic and ionic conductivities, diffusion and mass transport, and electron


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transfer and electrocatalysis. Due to their high surface areas, nanostructured materials can

support high electrode reaction rates, which should translate to high power capabilities.

Moreover, because such structures present reduced diffusion lengths, the time constant for

diffusion of active species can be brought down considerably. Although the high porosity of

such materials should facilitate ingress of electrolyte into the interior of the electrode

structure, it can reduce volumetric energy densities. Another disadvantage of nanostructured

electrode materials is that due to enhanced surface energies, they facilitate undesirable

reactions with the electrolyte, leading to extensive passivation, self-discharge, and truncated

cycling/calendar life. While nanoscopic materials do promise high-performing devices, their

suitability for energy storage hangs on our understanding of phenomena that occur at the

nanoscale.

It is clear that the ability to control matter at the nanoscale is becoming an additional

functional variable in our search for high-performance materials for electrochemical devices.

But that introduces more questions particularly relating to co-existence of nanoscale phases,

role of surface energy on electrochemical properties, electrolyte structure in confined spaces,

structure of surfaces at the nanoscale, effect of nano-dimensions on electronic properties,

delineation of pseudocapacitive behaviour from faradaic reactions at the nanoscale, and inter-

relationships between electron and ion transport in nanostructures.

8.2. Theory and modeling

In contrast to their simplicity in appearance, batteries and electrochemical capacitors are

complex systems with a multiplicity of reactive and passive components and interfaces. The

performance of the device is thus limited by their properties. A theoretical understanding of

the charge transfer phenomena in correlation with experimental results remains a large gulf

that must be bridged. There are also limitations brought about by mass and charge transport,

and their dependence on design and structural parameters. For example, the interplay of pore

size, pore morphology and pore distribution on mass/charge transport, and electrolyte

behavior in confined spaces are poorly understood. Modern analytical and characterization

tools, including in situ microscopic and spectroscopic tools, can help unravel the complex

molecular-level phenomena that underlie individual charge-transfer processes and the natureand properties of dynamically changing solid electrolyte interphases. Any insight thus gained


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on the working and failure mechanisms, backed by sound computational modeling and

simulation can lead to electrode materials, electrode architectures and system designs for

next-generation storage devices.

9. Technology readiness level

The technology readiness levels (TRL) of the different electrochemical storage systems can be

evaluated based on a metric as under.

(i)

innovation (TRL 1–3) [TRL 1: basic research; TRL 2: applied research; TRL 3:

critical function or proof-of-concept established].

(ii)

emerging technologies (TRL 4–6) [TRL 4: laboratory testing/validation of

component(s)/process(es); TRL 5: laboratory testing of integrated/semi-

integrated system; TRL 6: prototype system verified].

(iii)

system integration (TRL 7 and 8) [TRL 7: integrated pilot system

Table 2. Technology readiness levels for different electrochemical energy storage systems.

System Projected energy/power

density at system level

TRL Major issues/limitations

Advanced lead-acid 25–40 Wh/kg75–300 W/kg

>9 Low energy density.

Nickel–iron 30 Wh/kg

55 Wh/l

7 Gassing; low charging efficiency.

Iron–air 500 Wh/kg700 W/l

1–3

Nickel–metal hydride 70 Wh/kg

120 Wh/l

7–9

Lithium-ion 150–200 Wh/kg

250–300 Wh/l

7–9 Safety.

Lithium–sulfur 400 Wh/kg

600 Wh/l

4–6 Cycle life; polysulfide formation.

Sodium–sulfur 150–240 Wh/kg

150–130 Wh/l

7–9

ZEBRA 100–120 Wh/kg

150–200 Wh/l

7–9

Vanadium flow cell 10–25 Wh/l 7–8 Low volumetric energy density.

Soluble lead flow cell 5 Wh/l 4 Low energy efficiency.

Electrochemical double

layer capacitors

1–5 Wh/kg

100–2,000 W/kg

4-6

Supercapacitors 1–10 Wh/kg

1–2,000 W/kg

4-6

Lead–carbon hybrid 1–2 Wh/kg1,000 W/kg

4-6


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demonstrated; TRL 8: system incorporated in commercial design].

(iv)

market penetration (TRL 9) [TRL 9: system proven and ready for full

commercial deployment].

Under the aforesaid metric, the TRLs of the systems discussed above are indicated in Table

2, which factors in the current status of each technology and what can be achieved.

10. Recommendations

The committee after careful deliberations has made the following recommendations:

1. Establish an R&D programme, initially with an annual fund of Rs. 100 crore, to

support research projects in energy storage devices. The programme should fund

basic, directed basic and applied research projects at academic institutes,

universities and research institutes, both in public and private domains, as well as

public and private sector industries. In the academic institutes, the research

projects should specifically focus on high-risk basic and platform technologies,

whereas the industry should focus on technologies for commercialization,

ploughing in a part of its funds into research. As a general enabler, the government

should provide directions and funds for basic research, platform technologies,

infra-structure building, and even disruptive and tangential research. Multiple

funding with multiple approaches should be encouraged to provide a smorgasbord

of options to choose from. Efforts should be made to encourage an integrated

consortium approach with expertise drawn from seemingly disparate disciplines.

2. Establish centrally funded centers for research into select electrochemical energy

storage systems on a cooperative model of partnership with the industry, each

specializing on one system (iron-based accumulators, lead–carbon hybrid battery,

futuristic systems, supercapacitors). Besides developing specific technologies, each

centre shall act as a knowledge repository of developments in the specific area.

These centers shall work on a hub-and-spoke model, tapping on and benefiting

from discrete knowledge from across the country. Any generic knowledge

generated at the centers of battery research should be available to all. Intellectual

property rights should, however, is owned by the center, with the rightstransferred to the industry either on an exclusive or non-exclusive manner. A


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suitable model may be established for sharing the funding requirement of the

centers between industry and government. The Committee recommends

establishment of such centers at CECRI, Karaikudi (for iron-based accumulators),

IISc, Bangalore (for lead–carbon hybrid battery) and ARCI, Chennai (for lithium-

based batteries), with each center also pursuing activities on related supercapacitor

systems.

3. In view of the increasing growth and demand of lithium-ion batteries and the

absence of manufacturing facilities in the country, industries may be

encouraged to initially import the subcomponents, and to assemble and market.

The import of subcomponents may be exempted from duties to encourage

Indian industry to enter into manufacturing and progressively initiate

backward and forward integration. Such duty-free imports may be limited to a

specified period so that there will be pressure on the industry to quickly

implement the entire manufacturing proc

report on batteries 04072014

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